Three-component olefin polymerization catalyst containing an aluminum sesquihalide and a transition metal compound



United States Patent Ofi ice 3,004,015 Patented Oct. 10, 1961 3,004,015 THREE-COMPONENT OLEFIN POLYMERIZATION CATALYST CCNTAINING AN ALUMINUM SES- QUIHALIDE AND A TRANSITION METAL COM- POUND Harry W. Coover, Jr., and Newton H. Shearer, Jr., Kingsport, Tenn., assignors to Eastman Kodak Company, Rochester, N.Y., a corporation of New Jersey No Drawing. Filed Aug. 29, 1960, Ser. No. 52,338 16 Claims. (Cl. 26093.7)

This invention relates to a new and improved polymerization process and is particularly concerned with the use of a novel catalyst combination for preparing high molecular weight solid polyolefins, such as polypropylene, of high density and crystallinity. In a particular aspect the invention is concerned with the preparation of polypropylene and higher polyolefins having a high density using a particular catalyst combination which has unexpected catalytic activity and which gives products characterized by unusually high crystallinity, softening point, thermal stability, stiffness and being substantially free of non-crystalline polymers.

Polyethylene has heretofore been prepared by high pressure processes to give relatively flexible polymers having a rather high degree of chain branching and a density considerably lower than the theoretical density. Thus, pressures of the order of 500 atmospheres or more and usually of the order of 10001500 atmospheres are commonly employed. It has been found that more dense polyethylenes can be produced by certain catalyst combinations to give polymers which have very little chain branching and a high degree of crystallinity. The exact reason why certain catalyst combinations give these highly dense and highly crystalline polymers is not readily understood. Furthermore, the activity of the catalysts ordinarily depends upon certain specific catalyst combinations, and the results are ordinarily highly unpredictable, since relatively minor changes in the catalyst combination often lead to liquid polymers rather than the desired solid polymers.

Certain of the trialkyl aluminum compounds have been used in conjunction with inorganic halides to give high molecular weight polyethylene. Thus, triethyl aluminum in conjunction with titanium tetrachloride permits a low temperature, low pressure polymerization of ethylene to highly crystalline product. When this same aluminum triethyl is used in conjunction with a titanium tetraalkoxide, such as titanium tetrabutoxide, the mixture does not produce solid polyethylene for some reason which is not apparent.

Some of the catalysts that are eifective for producing crystalline high density polyethylene cannot be used to produce a similar type of polypropylene. For example, catalyst combinations of an alkyl aluminum sesquihalide with transition element compounds have been suggested for ethylene polymerization, but these catalysts are ineffective for polymerizing propylene to form high density crystalline polymers. Thus, one cannot predict whether a specific catalyst combination will be effective to produce crystalline high density polymers with specific a-olefins.

This invention is concerned with and has for an object the provision of improved processes whereby wmonoolefins and particularly propylene can be readily polymerized by catalytic means to give high molecular weight, highly crystalline polymers. A particular object of the invention is to provide an improved catalyst combination which has unexpected catalytic activity for the polymerization of a-monoolefins to form crystalline high density polymers. Other objects will be apparent from the description and claims which follow.

The above and other objects are attained by means of this invention, wherein a-monoolefins, either singly or in admixture, are readily polymerized to high molecular weight solid polymers by eflecting the polymerization in the presence of a catalytic mixture containing an aluminum sesquihalide having the formula Al R X wherein R is selected from the group consisting of alkyl radicals containing from 1 to 12 atoms, phenyl and benzyl and X is a halide selected from the group consisting of chlorine, bromine and iodine, a compound of a transition metal selected from the group consisting of titanium, zirconium, vanadium, chromium and molybdenum, and a stibine compound having the formula R Sb wherein each R is selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl. Among these hydrocarbon radicals are methyl, ethyl, propyl, butyl, phenyl, phenylethyl and naphthyl. In the stibine compound the three radicals represented by R can be the same or different. The catalytic activity of this mixture was wholly unexpected, particularly since mixtures of aluminum sesquihalides either singly or in admixture with transition element compounds had not been known to possess catalytic activity for the polymerization of propylene and higher olefins to crystalline polymers, and the third component of the catalyst is not a polymerization catalyst. The inventive process is carried out in liquid phase in an inert organic liquid and preferably an inert liquid hydrocarbon vehicle. The process proceeds with excellent results over a tempera ture range of from 0 C. to 250 C., although it is pre ferred to operate within the range of from about 50 C. to about 150 C. Likewise, the reaction pressures may be varied widely from about atmospheric pressure to very high pressures of the order of 20,000 p.s.i. or higher. pressures of the order of 30 to 1000 psi. give excellent results, and it is not necessary to employ the extremely high pressures which were necessary heretofore. The liquid vehicle employed is desirably one which serves as an inert reaction medium.

The invention is of particular importance in the preparation of highly crystalline polypropylene, the polybutenes and polystyrene although it can be used for polymerizing ethylene, mixtures of ethylene and propylene as well as other a-monoolefins containing up to 10 carbon atoms. The polyethylene which is obtained in accordance with this invention has a softening or fusion point greater than 120 C. whereby the products prepared therefrom can be readily employed in contact with boiling water without deformation or other deleterious effects. The process of the invention readily results in solid polymers having molecular weights greater than 1000 and usually greater than 10,000. Furthermore, polymers having molecular weights of as much as 1,000,000 or higher can be readily prepared if desired. The high molecular Weight, high density polyethylenes of this invention are insoluble in solvents at ordinary temperatures but they are soluble in such solvents as xylene, toluene or' tetralin at temperatures above 100 C. These solubility polyethylenes obtained by this process average close to A particular advantage of the invention is that,

of the order of 0.5 or lower. The densities are of the order of 0.945 or higher, with densities of the order of 0.96 or higher being obtained in many cases. The inherent viscosity as measured in tetralin at 145 C. can be varied from about 0.5 or lower to 5.0 or higher. Melt indices as measured by the standard ASTM method may be varied from about 0.1 to 100 or even higher.

The novel catalysts described above are quite useful for polymerizing propylene to form a crystalline, highdensity polymer. The polypropylene produced has a softening point above 155 C. and a density of 0.91 and higher. Usually, the density of the polypropylene is of the order of 0.91 to 0.92.

The polyolefins prepared in accordance with the invention can be molded or extruded and can be used to form plates, sheets, films, or a variety of molded objects which exhibit a higher degree of stiffness than do the corresponding high pressure polyolefins. The products can be extruded in the form of pipe or tubing of excellent rigidity and can be injection molded into a great variety of articles. The polymers can also be cold drawn into ribbons, bands, fibers or filaments of high elasticity and rigidity. Fibers of high strength can be spun from the molten polyolefins obtained according to this process.

As has been indicated above the improved results obtained in accordance with this invention depend upon the particular catalyst combination. Thus, one of the components of the catalyst is an aluminum sesquihalide having the formula Al R X wherein R is selected from the group consisting of alkyl radicals containing from 1 to 12, preferably from 1 to 4, carbon atoms, for example, methyl, ethyl, propyl, butyl, and the like, phenyl and benzyl, and X is a halogen selected from the group consisting of chlorine, bromine and iodine. The preferred aluminum sesquihalides are the lower alkyl aluminum sesquihalides and the most preferred compound is ethyl aluminum sesquihalide. Another component of the catalyst composition is a compound of a transition metal selected from the group consisting of titanium, zirconium, vanadium, chromium and molybdenum. In these compounds the transition metal can be at its maximum valence but it is possible to employ a compound of a transition metal having a reduced valence. Among the transition metal compounds that can be used are the halides, alkoxides, alkoxyhalidm and acetylacetonates of the above-named transition metals. In the alkoxides and alkoxyhalides the alkyl groups contain from 1 to 12 carbon atoms. Such compounds as titanium tetrachloride, titanium trichloride, titanium dichloride, titanium ethoxide, titanium butoxide, dibutoxy titanium dichloride, diethoxy titanium dichloride and titanium acetylacetonate can be used in the catalyst combinations. Similar compounds of zirconium, vanadium, chromium and molybdenum can also be used. For the most desirable results it is preferred to use a halide of titanium having either its maximum valency or a reduced valency and specifically it is preferred to employ either titanium tetrachloride or titanium trichloride in the catalyst composition. The third component of the catalyst composition is a stibine compound having the structural formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl. In this third component the R radicals can be the same but in some instances it is desired to employ different radicals within the definition set forth above. Among the specific compounds that can be used are tributylstibine, triethylstibine, trioctylstibine, triphenylstibine and the like.

The limiting factor in the temperature of the process appears to be the decomposition temperature of the catalyst. Ordinarily temperatures from 50 C. to 150 C- are employed although temperaturesas low as C. or as high as 250 C. can be employed if desired. Usually, it is not desirable or economical to effect the polymerization at temperatures below 0 C., and the process can be readily controlled at room temperature or higher which is an advantage from the standpoint of commercial processing. The pressure employed is usually only sufiicient to maintain the reaction mixture in liquid form during the polymerization, although higher pressures can be used if desired. The pressure is ordinarily achieved by pressuring the system with the monomer whereby additional monomer dissolves in the reaction vehicle as the polymerization progresses.

The polymerization embodying the invention can be carried out batchwise or in a continuous flowing stream process. The continuous processes are preferred for economic reasons, and particularly good results are obtaincd using continuous processes wherein a polymerization mixture of constant composition is continuously and progressively introduced into the polymerization zone and the mixture resulting from the polymerization is continuously and progressively withdrawn from the polymerization zone at an equivalent rate, whereby the relative concentration of the various components in the polymerization zone remains substantially unchanged during the process. This results in formation of polymers of extremely uniform molecular weight distribution over a relatively narrow range. Such uniform polymers possess distinct advantages since they do not contain any substantial amount of the low molecular weight or high molecular weight formations which are ordinarily found in polymers prepared by batch reactions.

In the continuous flowing stream process, the temperature is desirably maintained at a substantially constant value within the preferred range in order to achieve the highest degree of uniformity. Since it is desirable to employ a solution of the monomer of relatively high concentration, the process is desirably effected under a pressure of from 30 to 1000 p.s.i. obtained by pressuring the system with the monomer being polymerized. The amount of vehicle employed can be varied over rather wide limits with relation to the monomer and catalyst mixture. Best results are obtained using a concentration of catalyst of from about 0.1% to about 2% by weight based on the weight of the vehicle. The concentration of the monomer in the vehicle will vary rather widely depending upon the reaction conditions and will usually range from about 2 to 50% by weight. For a solution type of process it is preferred to use a concentration from about 2 to about 10% by weight based on the weight of the vehicle, and for a slurry type of process higher concentrations, for example up to 40% and higher are preferred. Higher concentrations of monomer ordinarily increase the rate of polymerization, but concentrations about 5 to 10% by weight in a solution process are ordinarly less desirable because the polymer dissolved in the reaction medium results in a very viscous solution. This process also operates quite well in pure monomer with no hydrocarbon diluent present. Hydrogen may be added to reduce the molecular weight of the polyolefin produced;

The molar ratio of the aluminum sesquihalide to transition metal compound can be varied within the range of 120.5 to 1:2, and the molar ratio of aluminum sesquihalide to stibine compound can be varied within the range of 1:1 to 1:025, but it will be understood that higher and lower molar ratios are within the scope of this invention. A particularly effective catalyst contains one mole of transition metal compound and 0.5 mole of stibine compound per mole of aluminum sesquihalide. The polymerization time can be varied as desired and will usually be of the order of from 30 minutes to several hours in batch processes. Contact times from 1 to 4 hours are commonly employed in autoclave type reactions. When a continuous process is employed, the contact time in the polymerization zone can also be regulated as desired, and in some cases it is not necessary to employ reaction or contact times much beyond one-half to one hour since a cyclic system can be employed by precipitation of the polymer and return of the vehicle and unused catalyst to the charging zone wherein the catalyst can be replenished and additional monomer introduced.

The organic vehicle employed can be an aliphatic alkane or cycloalkane such as pentane, hexane, heptane or cyclohexane, or a hydrogenated aromatic compound such as tetrahydronaphthalene or decahydronaphthalene, or a high molecular weight liquid parafiin or mixture of parafiins which are liquid at the reaction temperature, or an aromatic hydrocarbon such as benzene, toluene, xylene, or the like, or a halogenated aromatic compound such as chlorobenzene, chloronaphthalene, or orthodichlorobenzene. The nature of the vehicle is subject to considerable variation, although the vehicle employed should be liquid under the conditions of reaction and relatively inert. The hydrocarbon liquids are desirably employed. Other solvents which can be used include ethyl benzene, isopropyl benzene, ethyl toluene, n-propyl benzene, diethyl benzenes, mono and dialkyl naphthalenes, n-pentane, n-octane, isooctane, methyl cyclohexane, and any of the other well-known inert liquid hydrocarbons. The diluents employed in practicing this invention can be advantageously purified prior to use in the polymerization reaction by contacting the diluent, for example in a distillation procedure or otherwise, with the polymerization catalyst to remove undesirable trace impurities. Also, prior to such purification of the diluent the catalyst can be contacted advantageously with polymerizable a-monoolefin.

The polymerization ordinarily is accomplished by merely admixing the components of the polymerization mixture, and no additional heat is necessary unless it is desired to effect the polymerization at an elevated tem perature in order to increase the solubility of polymeric product in the vehicle. When the highly uniform polymers are desired employing the continuous process wherein the relative proportions of the various com ponents are maintained substantially constant, the temperature is desirably controlled Within a relatively narrow range. This is readily accomplished since the solvent vehicle forms a high percentage of the polymerization mixture and hence can be heated or cooled to maintain the temperature as desired. I

-A particularly effective catalyst for polymerizing ethylene, propylene and other a-monoolefins in accordance with this invention is a mixture of ethyl aluminum sesquibromide, titanium trichloride and triphenylstibine. The importance of the various components of this reaction mixture is evident from the fact that a mixture of ethyl aluminum sesquibromide and titanium trichloride is inelfective for polymerizing propylene. However, when triphenyl phosphine or other group VA compound within the scope of this invention is added to the mixture the resulting catalyst composition is highly effective for polymerizing propylene to form a highly crystalline highdensity polymer. Similarly, a catalyst mixture containing ethyl aluminum sesquibromide and titanium tetrachloride can be used to polymerize propylene but the polymer formed contains mainly dimers, trimers and tetramers of propylene. When the polymerization is carried out using a similar catalyst to which triphenyl phosphine or other group VA compound within the scope of this invention has been added the product is a highly crystalline polymer of high density and high softening point.

The invention is illustrated by the following examples of certain preferred embodiments thereof.

Example 1 A stainless steel autoclave, inside a nitrogen-filled drybox was charged with two grams of catalyst composed of ethylaluminum sesquichloride, titanium trichloride, and

triphenylstibine in the molar ratio of 1:1:0.5. The auto clave was removed from the drybox, and 100 g. of liquid propylene was added. The autoclave was attached to a heated rocking apparatus and'rocked at C. for six hours. LA yield of '89 g. of solid polypropylene was ob tained. This product, after isolation and drying, had an inherent viscosity in tetralin of 4.2 and a crystalline melting point of 175-182 C.

Example 2 The procedure of Example 1 was followed, but the catalyst was composed of methylaluminum sesquibromide, titanium trichloride, and tributylstibine in the molar ratio of 1:O.5:0.25 respectively. A yield of 93 g. of polypropylene was obtained. This polymer had an inherent viscosity of 3.8 and crystalline melting point of 168-179 C.

Example 3 The procedure of Example 1 was followed, except that the triphenylstibine was replaced by diphenyldodecylstibine and the respective catalyst component ratios were 1 :12: 1. The monomer mixture of 50 g. of propylene with 50 g. of l-butene was used., The copolymer product, after six hours at 150 C., weighed 83 g. Analysis of the unreacted monomer indicated that the product was a copolymer containing 54% propylene and 46% l-butene units. The inherent viscosity of the copolymer was 3.6.

Example4 A clean, dry, 500 ml. pressure bottle was purged with dry nitrogen and in a nitrogen-filled drybox was charged With 2 g. of catalyst composed of phenylaluminum sesquichloride, titanium trichloride, and diphenylstibine in the molar ratio of 1:1:0.5. To this catalyst mixture was added g. of 4-methy1-l-pentene. The bottle was attached to a shaking apparatus and shaken at 70 C. for 8 hours. The liquid monomer was polymerized to such an extent that the contents of the bottle became a dry powder. The catalyst residues were removed from the polymer by washing with methanol. The product was 97 g. of highly crystalline poly (4-methyl-lpentene) which had an inherent viscosity of 2.8, and melted at 205 C.

Example5 The procedure of Example 4 was followed, but vanadium trichloride was used instead of titanium trichloride. The yield was 87 g. of poly (4-methyl-1- pentene) having an inherent viscosity of 1.8. Efl'ective catalysts were also obtained when ZrCl CrCl or M001 were used in place of VCl Example 6 The procedure of Example 4 was followed with dodecylaluminum sesquichloride, titanium tetrabromide and diphenylethylstibine. The monomer was B-methyI-I-butene. A yield of 86 g. of poly (3-methyl-1-butene) was ob tained. This product melted at 295 C., and had an inherent viscosity of 3.2.

Example 7 The procedure of Example '1 was followed, except 100 ml. benzene was used as a reaction medium, and the monomer was 100 g. of butadiene. A yield of 84 g. of polybutadiene was obtained. The infrared absorption spectrum of this product indicated that it contained 85- 90% trans-1,4 unsaturation and 10-15% cis-1,4 unsaturation, with a small amount of 1,2 additional products.

Example 10 A 500 ml. pressure bottle was charged with 100 ml. of dry n-heptane and 1 g. of a catalyst composed of ethylalurninum sesquiiodide, titanium tetrachloride, and trimethylstibine in a molar ratio of 1:l:0.5. The bottle was attached to a shaking mechanism, and connected to a reservoir of ethylene maintained at 40 p.s.i.g. The bottle was heated to 50 C. with shaking; after six hours, a yield of 50 g. of polyethylene was obtained. The density of this polymer was 0.958. It had an inherent viscosity of 2.1, and melted at 131 C.

Thus, by means of this invention polyolefins such as polyethylene and polypropylene are readily produced using a catalyst combination which, based on the knowledge of the art, would not be expected to be effective. The polymers thus obtained can be extruded, mechanically milled, cast or molded as desired. The polymers can be used as blending agents with the relatively more flexible high pressure polyethylenes to give any desired combination of properties. The polymers can also be blended with antioxidants, stabilizers, plasticizers, fillers, pigments, and the like, or mixed with other polymeric materials, waxes and the like. in general, aside from the relatively higher values for such properties as softening point, density, stiffness and the like, the polymers embodying this invention can be treated in similar manner to those obtained by other processes.

From the detailed disclosure of this invention it is quite apparent that in this polymerization procedure a novel catalyst, not suggested in prior art polymerization procedures, is employed. As a result of the use of this novel catalyst, it is possible to produce polymeric hydrocarbons, particularly polypropylene, having properties not heretofore obtainable. For example, polypropylene prepared in the presence of catalyst combination within the scope of this invention is substantially free of rubbery and oily polymers and thus it is not necessary to subject such polypropylene of this invention to extraction procedures in order to obtain a commercial product. Also, polypropylene produced in accordance with this invention possesses unexpectedly high crystallinity, an unusually high softening point and outstanding thermal stability. Such polypropylene also has a very high stilfness as a result of the unexpectedly high crystallinity. The properties imparted to polypropylene prepared in accordance with this invention thus characterize and distinguish this polypropylene from polymers prepared by prior art polymerization procedures.

The novel catalyst defined above can be used to produce high molecular weight crystalline polymeric hydrocarbons. The molecular weight of the polymers can be varied over a wide range by introducing hydrogen to the polymerization reaction. Such hydrogen can be introduced separately or in admixture with the olefin monomer. The polymers produced in accordance with this invention can be separated from the polymerization catalyst by suitable extraction procedures, for example, by washing with water or lower aliphatic alcohols, such as methanol.

The catalyst compositions have been described above as being effective primarily for the polymerization of ormonoolefins. These catalyst compositions can, however, be used for polymerizing other a-olefins, and it is not necessary to limit the process of the invention to monoolefins. Other a-olefins that can be used are butadiene, isoprene, 1,3-pentadiene and the like.

Although the invention has been described in considerable detail with reference to certain preferred embodiments thereof, variations and modifications can be effected within the spirit and scope of this invention as described hereinabove and as defined in the appended claims. This application is a continuation-impart of Serial No. 724,915, filed March 31, 1958 and now U.S. Patent No. 2,951,060.

We claim:

1. In a polymerization of a-olefinic hydrocarbon material to form solid crystalline polymer, the improve ment which comprises catalyzing the polymerization with a catalytic mixture of an aluminum sesquihalide having the formula AI R' X wherein R is selected from the group consisting of alkyl radicals containing from 1 to 12 carbon atoms, phenyl and benzyl and X is a halogen selected from the group consisting of chlorine, bromine and iodine, a compound of a transition metal selected from the group consisting of titanium, zirconium, vanadium, chromium and molybdenum, and a stibine having the formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl.

2. In the polymerization of at least one monoolefin from the group consisting of ethylene and propylene to form solid crystalline polymer, the improvement which comprises efiecting the polymerization in liquid dispersion in an inert organic liquid and in the presence of a catalytic mixture of a lower alkyl aluminum sesquihalide, a titanium halide, and a stibine having the formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl aryl and aralkyl.

3. In a polymerization of propylene to form solid crystalline polymer, the improvement which comprises etfecting the polymerization in liquid dispersion in an inert organic liquid and in the presence of a catalytic mixture having a molar ratio of a lower alkyl aluminum sesquihalide and a titanium halide of 1:0.5 to 1:2 and a molar ratio of said lower alkyl aluminum sesquihalide and a stibine having the formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl of 1:1 to 1:025.

4. In the polymerization of propylene to form solid crystalline polymer, the improvement which comprises effecting the polymerization in liquid dispersion in an inert organic liquid and in the presence of a catalytic mixture having a molar ratio of ethyl aluminum sesquibromide and titanium trichloride of 110.5 to 1:2 and a molar ratio of ethyl aluminum sesquibromide and triphenylstibine of 1:1 to 120.25.

5. In the polymerization of propylene to form solid crystalline polymer, the improvement which comprises etfecting the polymerization in liquid dispersion in an inert organic liquid and in the presence of a catalytic mixture having a molar ratio of ethyl aluminum sesquibrornide and titanium tetrachloride of 110.5 to 1:2 and a molar ratio of ethyl aluminum sesquibromide and triphenylstibine of 1:1 to 1:0.25.

6. In the polymerization of propylene to form solid crystalline polymer, the improvement which comprises effecting the polymerization in liquid dispersion in an inert liquid hydrocarbon vehicle and in the presence of a catalytic mixture having a molar ratio of ethyl aluminum sesquibromide and titanium trichloride of 120.5 to 1:2 and a molar ratio of ethyl aluminum sesquibromide and tributylstibine of 1:1 to 1:0.25.

7. In the polymerization of propylene to form solid crystalline polymer, the improvement which comprises effecting the polymerization in liquid dispersion in an inert liquid hydrocarbon vehicle and in the presence of a catalytic mixture having a molar ratio of ethyl aluminum sesquichloride and titanium trichloride of 120.5 to

1:2 and a molar ratio of ethyl aluminum sesquichloride and triethylstibine of 1:1 to 1:0.25.

8. In the polymerization of propylene to form solid crystalline polymer, the improvement which comprises effecting the polymerization in liquid dispersion in an inert liquid hydrocarbon vehicle and in the presence of a catalytic mixture having a molar ratio of ethylaluminum sesquiiodide and titanium trichloride of 120.5 to 1:2 and a molar ratio of ethyl aluminum sesquiiodide and tributylstibine of 1:1 to 1:0.25.

9. As a composition of matter, a polymerization catalyst containing an aluminum sesquihalide having the formula Al R' X wherein R' is selected from the group consisting of alkyl radicals containing from 1 to 12 carbon atoms, phenyl and benzyl and X is a halogen selected from the group consisting of chlorine, bromine and iodine, a compound of a transition metal selected fromthe group consisting of titanium, zirconium, vanadium, chromium and molybdenum, and a stibine having the formula R Sb wherein each R is a radical selec ed from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl.

10. As a composition of matter, a polymerization catalyst containing a lower alkyl aluminum sesquihalide, a titanium halide, and a compound of a stibine having the formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl.

11. As a composition of matter, a polymerization catalyst containing a molar ratio of a lower alkyl aluminum sesquihalide and a titanium halide of 1:05 to 1:2 and a molar ratio of said lower alkyl aluminum sesquihalide and a stibine having the formula R Sb wherein each R is a radical selected from the group consisting of hydrogen and hydrocarbon radicals containing 1 to 12 carbon atoms and selected from the group consisting of alkyl, aryl and aralkyl of 1:1 to 1:0.25.

12. As a composition of matter, a polymerization catalyst containing a molar ratio of ethyl aluminum sesquibromide and titanium trichloride of 120.5 to 1:2 and a molar ratio of ethyl aluminum sesquibromide and triphenylstibine of 1:1 to 1:0.25.

13. As a composition of matter, a polymerization catalyst containing a molar ratio of ethyl aluminum sesquibromide and titanium tetrachloride of 120.5 to 1:2 and a molar ratio of ethyl aluminum sesquibromide and triphenylstibine of 1:1 to 1:0.25.

14. As a composition of matter, a polymerization catalyst containing a molar ratio of ethyl aluminum sesquibromide and titanium trichloride of 1:05 to 1:2 and a molar ratio of ethyl aluminum se'squibromide and tributylstibine of 1:1 to 1:0.25.

15. As a composition of matter, a polymerization catalyst containing a molar ratio of ethyl aluminum sesquichloride and titanium trichloride of 1:05 to 1:2 and a molar ratio of ethyl aluminum sesquichloride and triethyl stibine of 1:1 to 1:0.25.

16. As a composition of matter, -a polymerization catalyst containing a molar ratio of ethylaluminum sesquiiodide and titanium trichloride of 1:05 to 1:2 and a molar ratio of ethyl aluminum sesquiiodide and tributylstibine of 1:1 to 1:0.25.

Coover et Aug. 30, 

1. IN A POLYMERIZATION OF A-OLEFINIC HYDROCARBON MATERIAL TO FORM SOLID CRYSTALLINE POLYMER, THE IMPROVEMENT WHICH COMPRISES CATALYZING THE POLYMERIZATION WITH A CATALYTIC MIXTURE OF AN ALUMINUM SESQUIHALIDE HAVING THE FORMULA AL2R''3X3 WHEREIN R'' IS SELECTED FROM THE GROUP CONSISTING OF ALKYL RADICALS CONTAINING FROM 1 TO 12 CARBON ATOMS, PHENYL AND BENZYL AND X IS A HALOGEN SELECTED FROM THE GROUP CONSISTING OF CHLORINE, BROMINE AND IODINE, A COMPOUND OF A TRANSISTION METAL SELECTED FROM THE GROUP CONSISTING OF TITANIUM, ZICRONIUM, VANADIUM, CHROMIUM AND MOLYBDENUM, AND A STIBINE HAVING THE FORMULA R3SB WHEREIN EACH R IS A RADICAL SELECTED FROM THE GROUP CONSISTING OF HYDROGEN AND HYDROCARBON RADICALS CONTAINING 1 TO 12 CARBON ATOMS AND SELECTED FROM THE GROUP CONSISTING OF ALKYL, ARYL AND ARALKYL. 